Field of the Invention
[0001] The present invention relates to electrostatographic toners and, in particular, to
crosslinked binder polymers useful for preparing toner particles.
Background of the Invention
[0002] Crosslinked polymeric materials have long been known as useful binders for electrostatographic
toners. Various types of crosslinked polymers, including vinyl, styryl, and acrylic
resins, as well as condensation polymers such as polyesters are disclosed in U.S.
Patent No. 3,938,992 and in Reissue Patent No. 31,072.
[0003] Other references describing toners formed from crosslinked polyesters are:
[0004] U.S. Patent No. 5,276,127, which describes a crosslinked polyester derived from at
least one member selected from the group consisting of tribasic and tetrabasic acid
components and trihydric and tetrahydric alcohol components and an aromatic or alicyclic
diol component in which at least one of the hydroxyl groups is a secondary group.
[0005] U.S. Patent No. 5,486,444, which describes a process for preparing a crosslinked
polyester by first forming a polyhydroxy functional polyester resin precursor, which
is then reacted with a dianhydride or diepoxy functional crosslinking component.
[0006] U.S. Patent No. 5,789,527, which describes a polyester resin formed by linking crosslinked
low-molecular weight polyesters through a dicarboxylic linking agent.
[0007] In addition to their usefulness for the production of toners, crosslinked polyesters
have found extensive use in various other applications, for example, the production
of thermosetting powder coating compositions. Such compositions are disclosed in,
for example, U.S. Patent No. 5,373,084, which describes the preparation of semicrystalline
polyester plasticizers from crosslinkable resins and a variety of crosslinking agents.
Among the types of crosslinking agents disclosed in this reference are hydroxyalkylamides,
epoxy materials, glycouril compounds, and unblocked or blocked isocyanates.
[0008] Commercial polyester crosslinking chemistries frequently involve materials that are
toxic or malodorous and, in addition, require in their preparation catalysts that
may adversely affect the triboelectric performance of the toner particles. Furthermore,
catalyzed processes often require an intimate knowledge of the materials and processes
used by suppliers in the preparation of toner ingredient precursors. It would be highly
desirable to have the ability to prepare crosslinked polyester toner binders using
non-toxic, odorless, low cost ingredients under relatively mild conditions that do
not require catalysts.
Summary of the Invention
[0009] The present invention is directed to a binder polymer composition for electrostatographic
toners that comprises a carboxysubstituted precursor polymer crosslinked by reaction
with an N,N,N'N'-tetrakis(2-hydroxyalkyl) bisamide compound of the structure

wherein R
1 is a substituted or unsubstituted alkylene group containing 1 to about 10 carbon
atoms and R
2 is H or an alkyl group containing 1 to about 6 carbon atoms.
Detailed Description of the Invention
[0010] Unless otherwise specifically stated, the terms "substituted" or "substituent" in
this specification are used to refer to any group or atom other than hydrogen. Also,
the term "group", when used to refer to a substituent that includes a substitutable
hydrogen, encompasses not only the substituent's unsubstituted form but also its form
substituted with any substituent or group that does not interfere with formation of
the precursor polymer or its subsequent reaction with the crosslinking agent.
[0011] The present invention relates to binder polymers for toners that are produced by
the reaction of a crosslinking agent comprising an N,N,N'N'-tetrakis(2-hydroxyalkyl)
bisamide compound with a carboxysubstituted precursor polymer, without the need for
triboelectrically altering catalysts. Most preferably, the carboxysubstituted precursor
polymers are polyesters that are the reaction products of fumaric acid with alkoxylated
Bisphenol A, which are crosslinked with a bisamide compound that preferably is N,N,N',N'-tetrakis(2-hydroxyethyl)succinamide,
N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide, N,N,N',N'-tetrakis(2-hydroxyethyl)sebacamide,
or N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide. The bisamide crosslinking agent is
employed in an amount preferably about 0.1 to about 5, more preferably, about 0.5
to about 3 weight percent of the amount of carboxysubstituted precursor polymer.
Two of the aforementioned N,N,N'N'-tetrakis(2-hydroxyalkyl)alkylenebisamides preferred
in the practice of the present invention are available from Ems-Chemie AG, Zurich,
Switzerland and are designated by the product names PRIMID® XL-552 and PRIMID® QM-1260.
The chemical structures of these materials are as shown below:

Preferred carboxysubstituted precursor polymers for the practice of the present invention
are polyesters bearing pendant and/or terminal carboxyl groups, as represented by
the following general formula:

wherein R
3 is a substituted or unsubstituted alkylene group containing 1 to about 6 carbon atoms
or a substituted or unsubstituted arylene group containing 6 to about 16 carbon atoms;
R
4 is a substituted or an unsubstituted alkylene group containing 1 to about 6 carbon
atoms, or a substituted or unsubstituted arylene, alkylenediarylene, or arylenedialkylene
group containing 6 to about 20 carbon atoms.
[0012] Representative R
3 groups include, for example, 1,2-ethanediyl, 1,2-ethenediyl, 1,4-butanediyl, hexamethylene,
1,4-phenylene, 1,3-phenylene, 4-carboxy-1,3-phenylene, 1,1,3-trimethyl-3- (4-phenylene)-5-yl,
2,6-naphthalenediyl, 5-hydroxy-1,3-phenylene, and 2-chloro-1,4-phenylene groups. Representative
R
4 groups include, for example, 1,2-ethanediyl, 2,2-dimethyl-1,3-propanediyl, 2-carboxy-2-methyl-1,3-propanediyl,
1,4-butanediyl, 1,4-cyclohexanedimethylene, hexamethylene, 2,2'-oxydiethylene, 4,4'-isopropylidenediphenylene,
and 1,4-phenylene groups.
[0013] The carboxysubstituted precursor polyesters may contain more than one R
3 and R
4 group and may also include the residue of a polyol or polyacid with a functionality
greater than 2, thus providing a branched structure.
[0014] A particularly preferred class of carboxysubstituted polyesters are reaction products
of fumaric acid, maleic acid, or maleic anhydride with a glycol. Preferably, the glycol
is an alkoxylated derivative of Bisphenol A, represented by the following general
structure:

wherein R is H or methyl, and x + y has a value 2.0 to 20.0. The glycol may be a
mixture containing both primary and secondary hydroxy substituents. Most preferably,
the carboxysubstituted polyester is derived from fumaric acid and propoxylated Bisphenol
A, where R is methyl and x + y = 2.2. This most preferred polyester is a branched
polymer resulting from hydro-alkoxy additions across the fumarate double bonds.
[0015] Another preferred group of carboxysubstituted precursor polymers are vinyl polymers,
represented by the following structural formula:

wherein X is H or methyl, Y is H, CO
2H, CO
2R
5, or CONHR
6, R
5 and R
6 each independently represents alkyl groups containing 1 to about 3 carbon atoms,
Z represents the residue(s) of any copolymerizable monomer(s), m and n are weight
percentages whose total is 100, and m has a value from about 0.01 to 100.0. Monomers
corresponding to Z can be, for example, olefinic, styrenic, acrylic, and methacrylic
monomers, and mixtures thereof.
[0016] A representative carboxysubstituted vinyl polymer is shown below:

[0017] Also in accordance with the present invention, a mixture of carboxysubstituted polyesters
or a mixture of carboxysubstituted vinyl polymers, or a mixture of one or more carboxysubstituted
polyesters with one or more carboxysubstituted vinyl polymers may be employed.
[0018] Various addenda may be added to the toner formulation. These addenda include but
are not restricted to materials such as colorants (either pigments or dyes), charge
control agents, waxes, and low surface energy additives.
[0019] Measurement of the rheological properties of a polymer is useful for determining
its suitability as a toner binder polymer, in particular, for forming a toner image
that is fixed to a paper receiver using a heated roll. Useful polymers have a viscosity,
as measured on a dynamic viscometer at 120°C and 1 radian/second , of preferably about
20 kpoise to about 200 kpoise, more preferably about 40 kpoise to about 140 kpoise.
[0020] Storage modulus is a measure of the elastic nature of a polymer and provides some
indication of the operating range of a heated roll without resulting in offset. Polymers
useful for toners should have a storage modulus of preferably at least about 20 kdyne/cm
2, more preferably, at least about 35 kdyne/cm
2.
[0021] Tan delta, which is the ratio of the loss modulus to the storage modulus, gives an
indication of the viscous vs the elastic characteristics of a polymer. For use in
toners, polymers preferably should have a tan delta value of less than about 2, more
preferably, of less than about 1.
[0022] The following examples are illustrative of the present invention:
Example 1 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide
at 0.5% crosslinking agent level
[0023] 47.76g of a propoxylated bisphenol-A fumarate polyester, available as 382ES-HMW from
Reichhold Chemicals, Inc., was dry-blended with 0.24g of N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide
( PRIMID® XL-552). The mixture was placed in a laboratory mixer, available from C.
W. Brabender, Inc., equipped with sigma blades that had been preheated to 235°C. The
mixing speed was set at 150 rpm, and total mixing time was 4 minutes. The rheology
of the polyester before and after crosslinking was determined on a dynamic viscometer,
available from Rheometrics, Inc., at 120°C and 1 radian/second:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 0.5% PRIMID® XL-552 |
59 |
38 |
1.22 |
Example 2 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide
at 1% crosslinking agent level
[0024] The same procedure as in Example 1 was used, except that 47.52g of the propoxylated
bisphenol-A fumarate polyester was mixed with 0.48g of PRIMID® XL-552. The rheology
of the polyester before and after crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 1% PRIMID® XL-552 |
115 |
92 |
0.74 |
Example 3 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide
at 3% crosslinking agent level
[0025] The same procedure as in Example 1 was used, except that 46.56g of the propoxylated
bisphenol-A fumarate polyester was mixed with 1.44g of PRIMID® XL-552. The rheology
of the polyester before and after crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 3% PRIMID® XL-552 |
129 |
127 |
0.21 |
Example 4 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide
at 0.5% crosslinking agent level
[0026] The same procedure as Example 1 was used except 47.76g of the propoxylated bisphenol-A
fumarate polyester was mixed with 0.24g PRIMID® QM-1260. The rheology of the polyester
before and after crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 0.5% PRIMID® QM-1260 |
54 |
31 |
1.38 |
Example 5 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide
at 1% crosslinking agent level
[0027] The same procedure as in Example 4 was used, except that 47.52g of the propoxylated
bisphenol-A fumarate polyester was mixed with 0.48g of PRIMID® QM-1260. The rheology
of the polyester after crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 1% PRIMID® QM-1260 |
93 |
74 |
0.76 |
Example 6 -- Crosslinking a carboxysubstituted 2,2-dimethyl-1,3-propylene terephthalate polyester
with N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide at 1% crosslinker level
[0028] The same procedure as in Example 1 was used, except that 47.52g of a carboxysubstituted
2,2-dimethyl-1,3-propylene terephthalate polyester, prepared by Ruco Polymers Inc.
and designated PE 2073, was mixed with 0.48g of PRIMID® XL-552. The rheology before
and after crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
47 |
11 |
4.00 |
Polyester after crosslinking with 1% PRIMID® XL-552 |
170 |
137 |
0.72 |
Example 7 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide
in an extruder at 0.5% crosslinker level
[0029] 9950g of propoxylated bisphenol-A fumarate polyester (382ES-HMW) was dry-blended
with 50g PRIMID® XL-552 and processed with a twin-screw co-rotating extruder Model
ZSK-30, available from Werner & Pfleiderer Corp. Feed rate was 10 kg/hr, screw speed
was 300 rpm, and zone temperature setpoints were: zone 1 - 93°C, zones 2-5 - 216°C.
The polyester before and after crosslinking was measured in the same manner as in
Example 1 to obtain the following results:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 0.5% PRIMID® XL-552 |
46 |
35 |
0.87 |
Example 8 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'- tetrakis(2-hydroxyethyl)adipamide
in an extruder at 1% crosslinker level
[0030] 9900g of propoxylated bisphenol-A fumarate polyester (382ES-HMW) was dry-blended
with 100g PRIMID® XL-552 and processed with the Model ZSK-30 twin-screw co-rotating
extruder. Feed rate was 10 kg/hr, screw speed was 300 rpm, and zone temperature setpoints
were: zone 1 - 93°C, zones 2-5 - 216°C. The polyester before and after crosslinking
was measured in the same manner as in Example 1, giving the following results:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 1% PRIMID®XL-552 |
81 |
71 |
0.55 |
Example 9 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide
in an extruder at 0.5% crosslinker level
[0031] 9950g of propoxylated bisphenol-A fumarate polyester (382ES-HMW) was dry-blended
with 50g PRIMID® QM-1260 and processed with the Model ZSK-30 twin-screw co-rotating
extruder. Feed rate was 10 kg/hr, screw speed was 300 rpm, and zone temperature setpoints
were: zone 1 - 93°C, zones 2-5 - 216°C. The polyester before and after crosslinking
was measured in the same manner as Example 1 to give the following results:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 0.5% PRIMID®QM-1260 |
46 |
30 |
1.18 |
Example 10 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide
in an extruder at 1% crosslinker level
[0032] 9900g of propoxylated bisphenol-A fumarate polyester (382ES-HMW) was dry-blended
with 100g PRIMID® QM-1260 and processed with the Model ZSK-30 twin-screw co-rotating
extruder. Feed rate was 10 kg/hr, screw speed was 300 rpm, and zone temperature setpoints
were: zone 1 - 93°C, zones 2-5 - 216°C. The polyester before and after crosslinking
was measured in the same manner as in Example 1:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.7 |
5.00 |
Polyester after crosslinking with 1% PRIMID®QM-1260 |
92 |
78 |
0.62 |
Example 11 -- Preparation of N,N,N',N'-tetrakis(2-hydroxyethyl)succinamide
[0033]

A mixture of 43.55g (0.25 mol) of diethyl succinate and 157.71 g (1.50 mol) of diethanolamine
was heated under nitrogen in a 140°C bath for 1.75 hr while collecting the ethanol
distillate. The excess diethanolamine was then distilled off at reduced pressure (1.2
mm) while heating in a 190°C bath. The oily residue was cooled, stirred with acetone,
and allowed to stand. The oil crystallized to a white solid, which was collected and
dried. The yield of product was 48.27 g (66.0 % of theory); mp = 89-91°C.
Example 12 -- Preparation of N,N,N',N'-tetrakis(2-hydroxyethyl)sebacamide
[0034] 
A mixture of 57.58g (0.25 mol) dimethyl sebacate and 157.71g (1.50 mol) of diethanolamine
was heated in a 140°C bath under nitrogen for 2.5 hrs while collecting the methanol
condensate. The reaction mixture was subsequently heated in a 200°C at reduced pressure
(1.5 mm) to distill off excess diethanolamine. The highly viscous oily residue was
dissolved in an equal volume of acetone and stirred overnight. The resulting crystalline
solid was collected, washed with acetone, and dried. The yield of product was 35.0
g (9.3% of theory); mp = 87-98°C.
Example 13 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'- tetrakis(2-hydroxyethyl)succinamide
at 1% crosslinking agent level
[0035] The same procedure as in Example 1 was used, except that 47.52g of a propoxylated
bisphenol-A fumarate polyester was mixed with 0.48g of N,N,N',N'-tetrakis(2-hydroxyethyl)succinamide,
prepared as described in Example 11. The rheology of the polyester before and after
crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.1 |
6.24 |
Polyester after crosslinking with 1% N,N,N',N'-tetrakis-(2-hydroxyethyl)succinamide |
133 |
97 |
0.93 |
Example 14 -- Crosslinking propoxylated bisphenol-A fumarate polyester with N,N,N',N'-tetrakis(2-hydroxyethyl)sebacamide
at 1% crosslinking agent level
[0036] The same procedure as in Example 1 was used, except that 47.52g of a propoxylated
bisphenol-A fumarate polyester was mixed with 0.48g of N,N,N',N'-tetrakis(2-hydroxyethyl)sebacamide,
prepared as described in Example 12. The rheology of the polyester before and after
crosslinking was:
Identification |
Viscosity
(kpoise) |
Storage Modulus
(kdyne/cm2) |
Tan
Delta |
Polyester before crosslinking |
19 |
3.1 |
6.24 |
Polyester after crosslinking with 1% N,N,N',N'-tetrakis (2-hydroxyethyl)sebacamide |
126 |
89 |
1.00 |
Example 15 -- Preparation of a toner
[0037] The crosslinked polymer of Example 8 was used to prepare a toner by melt-blending
the following ingredients on a two-roll mill for 15 minutes at 120°C: 30 grams of
the crosslinked polyester of Example 8, 2.4 grams of REGAL® 330 carbon black (from
Cabot Corp.), 0.6 gram of VISCOL® 550P polypropylene wax (from Sanyo Corp.), and 0.6
gram of BONTRON® E-84 charge control agent (from Orient Corp.).
The mixture was pulverized to a particle size of 7-12 microns using a fluid energy
mill.
[0038] A developer was prepared by shaking together for 10 minutes 1 gram of toner with
9 grams of a silicone-resin coated carrier. The triboelectric charge for this developer
was -22 µc/g.
Example 16 - Roller-fusing evaluation
[0039] The fixing properties of the toner prepared in Example 15 were determined by passing
toned sheets through a roller-fuser obtained from a Kodak EK-95 copier. The toner
exhibited excellent offset latitude and fusing quality.
The use of N,N,N'N'-tetra(2-hydroxyalkyl)alkylenebisamides as crosslinking agents
in accordance with the present invention offers several significant advantages, including
the following:
the crosslinking agents and crosslinked polyesters derived therefrom emit no objectionable
odors either neat or in toners and require no hazard warning labels
no special storage measures or handling precautions such as special breathing equipment,
eye protection or hand protection are required
the crosslinking reaction is not influenced by catalysts; therefore monitoring of
catalyst in the precursor polyester or the introduction of potentially triboelectrically
altering catalysts is not required
the effective equivalent molecular weight is low, which translates to relatively low
crosslinking agent levels on a weight basis
the PRIMID® crosslinking agents are low cost, commercially available materials that
are listed on the TSCA inventory
the PRIMID® crosslinking agents are low melting (∼120°C) materials, which contributes
to the formation of a more homogeneous crosslinked toner binder
relatively low temperatures are required to effect the crosslinking reaction
the reactants and crosslinked products are colorless, providing useful materials for
the preparation of variously colored toners
The invention has been described in detail with particular reference to certain preferred
embodiments thereof, but it is to be understood that variations and modifications
can be effected within the spirit and scope of the invention, which is defined by
the following claims.
1. A binder polymer composition for electrostatographic toners comprising:
a carboxysubstituted precursor polymer crosslinked by reaction with an N,N,N'N'-tetrakis(2-hydroxyalkyl)
bisamide compound having the structure

wherein R
1 is a substituted or unsubstituted alkylene group containing 1 to about 10 carbon
atoms and R
2 is H or an alkyl group containing 1 to about 6 carbon atoms.
2. The binder polymer composition of claim 1 wherein said N,N,N'N'-tetrakis(2-hydroxyalkyl)
bisamide compound is selected from the group consisting of N,N,N',N'-tetrakis(2-hydroxyethyl)succinamide,
N,N,N',N'-tetrakis(2-hydroxyethyl)adipamide, N,N,N',N'-tetrakis(2-hydroxyethyl)sebacamide,
and N,N,N',N'-tetrakis(2-hydroxypropyl)adipamide.
3. The binder polymer composition of claim 1 wherein said carboxysubstituted precursor
polymer comprises a polyester having the structure

wherein R
3 is a substituted or unsubstituted alkylene group containing 1 to about 6 carbon atoms
or a substituted or unsubstituted arylene group containing 6 to about 16 carbon atoms;
R
4 is a substituted or an unsubstituted alkylene group containing 1 to about 6 carbon
atoms, or a substituted or unsubstituted arylene, alkylenediarylene, or arylenedialkylene
group containing 6 to about 20 carbon atoms.
4. The binder polymer composition of claim 3 wherein R3 is selected from the group consisting of 1,2-ethanediyl, 1,2-ethenediyl, 1,4-butanediyl,
hexamethylene, 1,4-phenylene, 1,3-phenylene, 4-carboxy-1,3-phenylene, 1,1,3-trimethyl-3-(4-phenylene)-5-yl,
2,6-naphthalenediyl, 5-hydroxy-1,3-phenylene, 2-chloro-1,4-phenylene, and mixtures
thereof.
5. The binder polymer composition of claim 3 wherein R4 is selected from the group consisting of 1,2-ethanediyl, 2,2-dimethyl-1,3-propanediyl,
2-carboxy-2-methyl-1,4-butanediyl, 1,4-cyclohexanedimethylene, hexamethylene, 2,2'-oxydiethylene,
4,4'-isopropylidenediphenylene, 1,4-phenylene, and mixtures thereof.
6. The binder polymer composition of claim 3 wherein R
4 in said polyester is an alkoxylated Bisphenol A residue, said polyester being formed
from a glycol having the structure

wherein R is H or CH
3, and x + y has a value 2.0 to 20.0.
7. The binder polymer composition of claim 6 wherein R is CH3, and x + y = 2.2.
8. The binder polymer composition of claim 1 wherein said carboxysubstituted precursor
polymer comprises a vinyl polymer having the structure

wherein X is H or CH
3, Y is H, CO
2H, CO
2R
5, or CONHR
6, wherein R
5 and R
6 each independently represents an alkyl group containing 1 to about 3 carbon atoms,
Z represents the residue of at least one copolymerizable monomer, m and n are weight
percentages whose total is 100, and m has a value from about 0.01 to 100.0.
9. The binder polymer composition of claim 8 wherein said copolymerizable monomers are
selected from the group of olefinic, styrenic, acrylic, and methacrylic monomers,
and mixtures thereof.
10. The binder polymer composition of claim 8 wherein said vinyl polymer has the formula
11. The binder polymer composition of claim 1 wherein said carboxysubstituted precursor
polymer is selected from a mixture of carboxysubstituted polyesters, a mixture of
carboxysubstituted vinyl polymers, or a mixture of one or more carboxysubstituted
polyesters with one or more carboxysubstituted vinyl polymers.
12. The binder polymer composition of claim 1 wherein said carboxysubstituted precursor
polymer comprises a 2,2-dimethyl-1,3-propylene terephthalate polyester.
13. The binder polymer composition of claim 1 comprising said bisamide compound in an
amount about 0.1 to about 5 weight percent of the amount of said carboxysubstituted
precursor polymer.
14. The binder polymer composition of claim 13 comprising said bisamide compound in an
amount about 0.5 to about 3 weight percent of the amount of said carboxysubstituted
precursor polymer.
15. The binder polymer composition of claim 1 having a viscosity, as measured on a dynamic
viscometer at 120°C and 1 radian/second , of about 20 kpoise to about 200 kpoise.
16. The binder polymer composition of claim 15 having a viscosity, as measured on a dynamic
viscometer at 120°C and 1 radian/second, of about 40 kpoise to about 140 kpoise.
17. The binder polymer composition of claim 1 having a storage modulus of at least about
20 kdyne/cm2.
18. The binder polymer composition of claim 17 having a storage modulus of at least about
35 kdyne/cm2.
19. The binder polymer composition of claim 1 having a tan delta value of less than about
2.
20. The binder polymer composition of claim 19 having a tan delta value of less than about
1.
21. A toner composition comprising the binder polymer composition of claim 1.
22. A toner composition of claim 21 further comprising addenda selected from the group
consisting of pigments, dyes, charge control agents, waxes, low surface energy additives,
and combinations thereof.